JP6242289B2 - Refrigeration cycle equipment - Google Patents

Refrigeration cycle equipment Download PDF

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JP6242289B2
JP6242289B2 JP2014102941A JP2014102941A JP6242289B2 JP 6242289 B2 JP6242289 B2 JP 6242289B2 JP 2014102941 A JP2014102941 A JP 2014102941A JP 2014102941 A JP2014102941 A JP 2014102941A JP 6242289 B2 JP6242289 B2 JP 6242289B2
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refrigerant
pipe
heat exchanger
compressor
refrigeration cycle
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JP2015218954A (en
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裕一 庄司
裕一 庄司
浩平 葛西
浩平 葛西
美藤 尚文
尚文 美藤
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三菱電機株式会社
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本発明は、冷凍サイクル装置に関し、たとえば寒冷地向けの温水生成機である空気調和装置が有する冷媒回路に内部熱交換器を備えたものに関する。   The present invention relates to a refrigeration cycle apparatus, for example, a refrigerant circuit having an internal heat exchanger in a refrigerant circuit included in an air conditioner that is a hot water generator for cold regions.
従来の空気調和装置において、室内機と室外機とが冷媒配管で接続されており、冷媒配管の長さに応じて冷媒回路内の冷媒量を調整するものがある。この種の空気調和装置では、余剰冷媒を溜めるための圧力容器を備えている。   In some conventional air conditioners, an indoor unit and an outdoor unit are connected by a refrigerant pipe, and the refrigerant amount in the refrigerant circuit is adjusted according to the length of the refrigerant pipe. This type of air conditioner includes a pressure vessel for storing excess refrigerant.
また、過冷却度の効率的な確保を目的に、冷媒回路内の圧縮機の吸入前に設けられたアキュムレータに、凝縮器後の配管を接続したことを特徴とする空気調和装置がある(たとえば、特許文献1参照)。   In addition, there is an air conditioner characterized by connecting a pipe after a condenser to an accumulator provided before suction of a compressor in a refrigerant circuit for the purpose of efficiently ensuring the degree of supercooling (for example, , See Patent Document 1).
特開平9−152204号公報(たとえば、[0031]〜[0034]、図3、図4参照)Japanese Patent Laid-Open No. 9-152204 (see, for example, [0031] to [0034], FIG. 3 and FIG. 4)
特許文献1に記載されているような従来の空気調和装置は、寒冷地で使用される場合は室外機が低外気温で使用されることが多く、圧縮機の吸入過熱度を確保できずに冷媒が圧縮機へ液バックして、圧縮機の故障を引き起こしてしまうという課題があった。   In the conventional air conditioner described in Patent Document 1, when used in a cold region, the outdoor unit is often used at a low outdoor temperature, and the suction superheat degree of the compressor cannot be ensured. There was a problem that the refrigerant liquid-backed to the compressor, causing a compressor failure.
また、寒冷地では冷媒と水とを熱交換する凝縮器で水を高温にすることが求められるため、凝縮温度を高く設定する必要がある。しかし、凝縮温度を高く設定すると凝縮器の出入口間のエンタルピー差が減少し、暖房能力が低下してしまう。そこで、性能低下を抑制するため、十分な過冷却度を確保する必要があった。   In cold districts, it is required to set the water to a high temperature with a condenser that exchanges heat between the refrigerant and water, and therefore the condensation temperature must be set high. However, if the condensation temperature is set high, the enthalpy difference between the inlet and outlet of the condenser is reduced, and the heating capacity is reduced. Therefore, it was necessary to ensure a sufficient degree of supercooling in order to suppress the performance degradation.
また、冷媒配管の長さや運転状態の違いによって生じる冷媒回路内の冷媒量の変化に対応できるように、大型の圧力容器を備える必要があるが、大きなスペースが必要となる。そのため、室内機が大型化してしまい、材料費のコストアップ、室外機の重量増加による輸送費のコストアップなどを招いてしまうという課題があった。   Moreover, although it is necessary to provide a large pressure vessel so as to be able to cope with the change in the refrigerant amount in the refrigerant circuit caused by the difference in the length of the refrigerant pipe and the operating state, a large space is required. For this reason, the indoor unit is increased in size, and there is a problem in that the cost of material is increased and the cost of transportation is increased due to an increase in the weight of the outdoor unit.
本発明は、以上のような課題のうち少なくとも一つを解決するためになされたもので、過冷却度と過熱度を効果的に確保して、暖房性能低下と圧縮機への液バックを抑制することができる冷凍サイクル装置を提供することを目的としている。   The present invention has been made to solve at least one of the problems as described above, and effectively secures the degree of supercooling and the degree of superheat, thereby suppressing heating performance deterioration and liquid back to the compressor. It is an object of the present invention to provide a refrigeration cycle apparatus that can be used.
本発明に係る冷凍サイクル装置は、圧縮機、流路切換手段、凝縮器、絞り機構、および蒸発器が冷媒配管で順次接続され、冷媒が循環する冷媒回路を備え、該冷媒回路は、前記凝縮器から前記絞り機構へ向かう冷媒と、前記蒸発器から前記圧縮機へ向かう冷媒とを、対向流で熱交換する内部熱交換器を備え、該内部熱交換器は、内管と外管とからなる二重管構造を有し、前記内管は前記凝縮器と前記絞り機構との間に接続され、前記外管は前記蒸発器と前記圧縮機との間に接続され、前記内管の下部に、液冷媒が溜まる液溜め部が設けられており、前記液溜め部は、鉛直方向下方に凹んだU字形状を有するものである。 A refrigeration cycle apparatus according to the present invention includes a refrigerant circuit in which a compressor, a flow path switching unit, a condenser, a throttling mechanism, and an evaporator are sequentially connected by a refrigerant pipe, and the refrigerant circulates. An internal heat exchanger for exchanging heat in a counter flow between the refrigerant going from the evaporator to the throttle mechanism and the refrigerant going from the evaporator to the compressor, the internal heat exchanger from the inner pipe and the outer pipe The inner pipe is connected between the condenser and the throttling mechanism, the outer pipe is connected between the evaporator and the compressor, and the lower part of the inner pipe In addition, a liquid storage part for storing liquid refrigerant is provided, and the liquid storage part has a U-shape that is recessed downward in the vertical direction .
本発明に係る冷凍サイクル装置によれば、冷媒回路に内部熱交換器を備え、凝縮器から絞り機構へ向かう冷媒と、蒸発器から圧縮機へ向かう冷媒とを、対向流で熱交換させることで、過冷却度と過熱度を効果的に確保して、暖房性能低下と圧縮機への液バックを抑制することができる。   According to the refrigeration cycle apparatus according to the present invention, an internal heat exchanger is provided in the refrigerant circuit, and heat is exchanged between the refrigerant from the condenser toward the throttle mechanism and the refrigerant from the evaporator toward the compressor in a counterflow. Thus, it is possible to effectively secure the degree of supercooling and the degree of superheat, and to suppress heating performance deterioration and liquid back to the compressor.
本発明の実施の形態に係る冷凍サイクル装置の冷媒回路図である。It is a refrigerant circuit figure of the refrigerating cycle device concerning an embodiment of the invention. 図1に示す内部熱交換器の断面図である。It is sectional drawing of the internal heat exchanger shown in FIG. 本発明の実施の形態に係る冷凍サイクル装置のモリエル線図である。It is a Mollier diagram of the refrigerating cycle device concerning an embodiment of the invention.
以下、本発明の実施の形態を図面に基づいて説明する。なお、以下に説明する実施の形態によって本発明が限定されるものではない。また、以下の図面では各構成部材の大きさの関係が実際のものとは異なる場合がある。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. The present invention is not limited to the embodiments described below. Moreover, in the following drawings, the relationship of the size of each component may be different from the actual one.
実施の形態.
図1は、本発明の実施の形態に係る冷凍サイクル装置の冷媒回路図である。
本実施の形態では、冷凍サイクル装置として寒冷地向けの温水生成機である空気調和装置1を例に説明する。
空気調和装置1は、図1に示すように室外機2と水が流れる水配管3とを備えている。
室外機2は、圧縮機4、四方弁5、凝縮器であるプレート式熱交換器6、電子膨張弁8、および蒸発器9が冷媒配管で環状に順次接続され、冷媒が循環する冷媒回路を備えている。
Embodiment.
FIG. 1 is a refrigerant circuit diagram of a refrigeration cycle apparatus according to an embodiment of the present invention.
In the present embodiment, an air conditioner 1 that is a hot water generator for cold regions will be described as an example of a refrigeration cycle apparatus.
As shown in FIG. 1, the air conditioner 1 includes an outdoor unit 2 and a water pipe 3 through which water flows.
The outdoor unit 2 includes a refrigerant circuit in which a compressor 4, a four-way valve 5, a plate heat exchanger 6 that is a condenser, an electronic expansion valve 8, and an evaporator 9 are sequentially connected in an annular manner through a refrigerant pipe, and the refrigerant circulates. I have.
なお、四方弁5は冷媒の流路を切り換えるためのものであるが、四方弁5に代えて二方弁や三方弁などを用いて流路を切り換えてもよい。
また、四方弁5は本発明の「流路切換手段」に相当する。
Although the four-way valve 5 is for switching the refrigerant flow path, the flow path may be switched using a two-way valve, a three-way valve or the like instead of the four-way valve 5.
The four-way valve 5 corresponds to the “flow path switching means” of the present invention.
また、プレート式熱交換器6には水配管3が接続されており、プレート式熱交換器6において冷媒と水とが熱交換するように構成されている。   A water pipe 3 is connected to the plate heat exchanger 6, and the plate heat exchanger 6 is configured to exchange heat between refrigerant and water.
また、プレート式熱交換器6と電子膨張弁8との間、かつ、四方弁5と圧縮機4の吸入側との間には内部熱交換器7が設けられており、プレート式熱交換器6から電子膨張弁8へ向かう冷媒と、蒸発器9から圧縮機4へ向かう冷媒とを、対向流で熱交換するように構成されている。   Further, an internal heat exchanger 7 is provided between the plate heat exchanger 6 and the electronic expansion valve 8 and between the four-way valve 5 and the suction side of the compressor 4, and the plate heat exchanger Heat is exchanged between the refrigerant directed from 6 to the electronic expansion valve 8 and the refrigerant directed from the evaporator 9 to the compressor 4 in a counterflow.
なお、凝縮器はプレート式熱交換器6に限定されず、他の熱交換器を用いてもよい。
また、電子膨張弁8は本発明の「絞り機構」に相当する。
In addition, a condenser is not limited to the plate-type heat exchanger 6, You may use another heat exchanger.
The electronic expansion valve 8 corresponds to the “throttle mechanism” of the present invention.
図2は、図1に示す内部熱交換器7の断面図である。
本実施の形態に係る内部熱交換器7は、内管10と外管11とからなる3セットの二重管構造を有し、内管10は凝縮器であるプレート式熱交換器6と電子膨張弁8との間に接続され、外管11は四方弁5と圧縮機4の吸入側との間に接続される。
FIG. 2 is a cross-sectional view of the internal heat exchanger 7 shown in FIG.
The internal heat exchanger 7 according to the present embodiment has a three-set double tube structure composed of an inner tube 10 and an outer tube 11, and the inner tube 10 includes a plate heat exchanger 6 that is a condenser and an electronic device. The outer pipe 11 is connected between the expansion valve 8 and the four-way valve 5 and the suction side of the compressor 4.
内管10には、外径が9.52mmの配管が用いられており、外管11には、一辺の長さが20cmで外径が15.88mmの配管が用いられている。
また、内管10の下部は、液冷媒を溜めるU字形状の液溜め部12が設けられており、一辺の長さが20cmで外径が15.88mmの配管を180°曲げて形成されている。液溜め部12の上方には、内管10同士を接続してガス冷媒が通過する分配管13が設けられており、外径は4.8mmである。
A pipe having an outer diameter of 9.52 mm is used for the inner pipe 10, and a pipe having a side length of 20 cm and an outer diameter of 15.88 mm is used for the outer pipe 11.
The lower part of the inner tube 10 is provided with a U-shaped liquid reservoir 12 for storing liquid refrigerant, which is formed by bending a pipe having a side length of 20 cm and an outer diameter of 15.88 mm by 180 °. Yes. Above the liquid reservoir 12, there is provided a distribution pipe 13 that connects the inner pipes 10 and through which the gas refrigerant passes, and has an outer diameter of 4.8 mm.
図3は、本発明の実施の形態に係る冷凍サイクル装置のモリエル線図である。
以下、暖房運転時の冷媒の流れについて図3を用いて説明する。
圧縮機4から吐出された高温高圧のガス冷媒(A点)は、四方弁5を介して凝縮器であるプレート式熱交換器6を通過し、その際に水配管3を流れる水と熱交換し、その水に放熱して高温高圧の液冷媒(B点)となる。
FIG. 3 is a Mollier diagram of the refrigeration cycle apparatus according to the embodiment of the present invention.
Hereinafter, the flow of the refrigerant during the heating operation will be described with reference to FIG.
The high-temperature and high-pressure gas refrigerant (point A) discharged from the compressor 4 passes through the plate-type heat exchanger 6 that is a condenser through the four-way valve 5 and exchanges heat with water flowing through the water pipe 3 at that time. Then, it dissipates heat to the water and becomes a high-temperature and high-pressure liquid refrigerant (point B).
その後、内部熱交換器7の構成部品の1つである内管10を通過するが、その際に外管11を流れる冷媒と熱交換し、その冷媒に放熱して過冷却される(C点)。
その後、電子膨張弁8で減圧された高温低圧の液冷媒(D点)は、蒸発器9を通過し、その際に空気と熱交換し、その空気から吸熱して低温低圧のガス冷媒(E点)となる。
After that, it passes through the inner pipe 10 which is one of the components of the internal heat exchanger 7, but at that time, it exchanges heat with the refrigerant flowing in the outer pipe 11, and dissipates heat to the refrigerant and is supercooled (point C). ).
Thereafter, the high-temperature and low-pressure liquid refrigerant (point D) decompressed by the electronic expansion valve 8 passes through the evaporator 9, exchanges heat with the air at that time, absorbs heat from the air, and low-temperature and low-pressure gas refrigerant (E Point).
その後、四方弁5を介して内部熱交換器7の構成部品の1つである外管11を通過するが、その際に内管10を流れる冷媒と熱交換し、その冷媒から吸熱して過熱された後(F点)、圧縮機4に戻る。   After that, it passes through the outer pipe 11 which is one of the components of the internal heat exchanger 7 through the four-way valve 5, but at that time, heat exchange with the refrigerant flowing through the inner pipe 10 is performed, and heat is absorbed from the refrigerant to overheat. After that (point F), the process returns to the compressor 4.
以上のように、凝縮器であるプレート式熱交換器6と電子膨張弁8との間に接続される内部熱交換器7の内管10を流れる高温の冷媒と、四方弁5と圧縮機4の吸入側との間に接続される外管11を流れる低温の冷媒とを対向流で熱交換させる。   As described above, the high-temperature refrigerant flowing through the inner pipe 10 of the internal heat exchanger 7 connected between the plate heat exchanger 6 that is a condenser and the electronic expansion valve 8, the four-way valve 5, and the compressor 4. The low-temperature refrigerant flowing through the outer pipe 11 connected between the suction side and the suction side is heat-exchanged in a counterflow.
そうすることで、図3に示すように凝縮器であるプレート式熱交換器6出口の過冷却度(SC)を確保して暖房性能の向上を図ることができる。また、圧縮機4の吸入過熱度(SH)を確保して圧縮機4への液バックを抑制し、信頼性の向上を図ることができる。   By doing so, as shown in FIG. 3, the degree of supercooling (SC) at the outlet of the plate heat exchanger 6 that is a condenser can be ensured and the heating performance can be improved. Moreover, the suction superheat degree (SH) of the compressor 4 can be ensured, the liquid back to the compressor 4 can be suppressed, and the reliability can be improved.
従来の空気調和装置では、冷媒が循環する冷媒回路を室内機と室外機とで構成しているため、室外機と室内機との組み合わせや接続する冷媒配管の長さによって余剰冷媒量が多く発生してしまう。そのため、その余剰冷媒を溜めることができる大型の圧力容器が必要となる。   In a conventional air conditioner, the refrigerant circuit in which the refrigerant circulates is composed of an indoor unit and an outdoor unit, so a large amount of excess refrigerant is generated depending on the combination of the outdoor unit and the indoor unit and the length of the refrigerant pipe to be connected. Resulting in. Therefore, a large pressure vessel capable of storing the excess refrigerant is required.
しかし、本実施の形態に係る空気調和装置1によれば、冷媒が循環する冷媒回路を室外機2のみで構成しているため、冷媒配管の長さが変化せず、冷媒回路内の冷媒量が変化しない。   However, according to the air conditioner 1 according to the present embodiment, since the refrigerant circuit in which the refrigerant circulates is configured only by the outdoor unit 2, the length of the refrigerant pipe does not change, and the refrigerant amount in the refrigerant circuit Does not change.
そのため、冷房運転、暖房運転などの運転状態の違いで発生する余剰冷媒のみを溜めることができるように内部熱交換器7の構造を工夫することで、圧力容器が不要となる。   Therefore, a pressure vessel becomes unnecessary by devising the structure of the internal heat exchanger 7 so that only surplus refrigerant generated due to a difference in operating state such as cooling operation and heating operation can be stored.
そして、(大型の)圧力容器が不要であるため、室外機2を小型化でき、材料費のコストダウン、室外機2の重量低下による輸送費のコストダウンなどを実現することができる。   And since the (large) pressure vessel is unnecessary, the outdoor unit 2 can be reduced in size, the material cost can be reduced, and the transportation cost can be reduced due to the weight reduction of the outdoor unit 2.
本実施の形態に係る空気調和装置1の室外機2では、冷房運転時の方が暖房運転時と比べて多くの冷媒を必要とする。これは、プレート式熱交換器6が鉄板で作られてBOX形状をしていることと、冷房運転時には低圧液状態で冷媒が入ってくることに起因してプレート式熱交換器6内に液冷媒が溜まりやすくなるためであり、冷媒量の差は最大で683ccとなる。   In the outdoor unit 2 of the air conditioning apparatus 1 according to the present embodiment, the cooling operation requires more refrigerant than the heating operation. This is because the plate heat exchanger 6 is made of iron plate and has a BOX shape, and the refrigerant enters the plate heat exchanger 6 in the low pressure liquid state during the cooling operation. This is because the refrigerant tends to accumulate, and the maximum difference in the refrigerant amount is 683 cc.
本実施の形態では、内部熱交換器7の内管10同士を繋ぐ配管には180°曲げた外径15.88mmのものを使用しており、配管の肉厚1.0mmとして計算すると図2に示す2ヶ所の液溜め部12の容積の合計は695ccとなり、暖房運転時に発生する余剰冷媒を溜めることが可能となる。   In the present embodiment, the pipe connecting the inner pipes 10 of the internal heat exchanger 7 uses a pipe having an outer diameter of 15.88 mm bent by 180 °. The total volume of the two liquid reservoirs 12 shown in FIG. 4 becomes 695 cc, and it is possible to store excess refrigerant generated during heating operation.
また、液溜め部12の上方に内管10同士を接続する分配管13を設けることにより、液溜め部12に液冷媒が溜まった状態でガス冷媒を通過させることができる。そして、溜まった余剰の液冷媒は電子膨張弁8の開度を調整することで冷媒回路内を循環する冷媒量の増減に利用され、温度センサ(図示せず)により検知される過冷却度が最適な値となるように制御される。   Further, by providing the distribution pipe 13 that connects the inner pipes 10 to each other above the liquid reservoir 12, the gas refrigerant can be passed in a state where the liquid refrigerant is accumulated in the liquid reservoir 12. The excess liquid refrigerant accumulated is used to increase or decrease the amount of refrigerant circulating in the refrigerant circuit by adjusting the opening of the electronic expansion valve 8, and the degree of supercooling detected by a temperature sensor (not shown) is increased. It is controlled so as to be an optimum value.
以上のように、本実施の形態に係る空気調和装置1によれば、内部熱交換器7の内管10を流れる高温の冷媒と、外管11を流れる低温の冷媒とを対向流で熱交換させることで、図3に示すように凝縮器であるプレート式熱交換器6出口の過冷却度を確保して暖房性能の向上を図ることができる。また、圧縮機4の吸入過熱度を確保して圧縮機4への液バックを抑制し、信頼性の向上を図ることができる。   As described above, according to the air conditioning apparatus 1 according to the present embodiment, heat exchange is performed between the high-temperature refrigerant flowing through the inner pipe 10 of the internal heat exchanger 7 and the low-temperature refrigerant flowing through the outer pipe 11 in a counterflow. By doing so, as shown in FIG. 3, the degree of supercooling at the outlet of the plate heat exchanger 6 that is a condenser can be ensured and the heating performance can be improved. Further, the degree of suction superheat of the compressor 4 can be ensured, the liquid back to the compressor 4 can be suppressed, and the reliability can be improved.
また、アキュムレータやレシーバなどの(大型の)圧力容器が不要であるため、室外機2を小型化でき、材料費のコストダウン、室外機2の重量低下による輸送費のコストダウンなどを実現することができる。   Moreover, since a (large) pressure vessel such as an accumulator or a receiver is not required, the outdoor unit 2 can be reduced in size, material costs can be reduced, and transportation costs can be reduced due to a decrease in the weight of the outdoor unit 2. Can do.
1 空気調和装置、2 室外機、3 水配管、4 圧縮機、5 四方弁、6 プレート式熱交換器、7 内部熱交換器、8 電子膨張弁、9 蒸発器、10 内管、11 外管、12 液溜め部、13 分配管。   DESCRIPTION OF SYMBOLS 1 Air conditioning apparatus, 2 outdoor unit, 3 water piping, 4 compressor, 5 4-way valve, 6 plate type heat exchanger, 7 internal heat exchanger, 8 electronic expansion valve, 9 evaporator, 10 inner pipe, 11 outer pipe , 12 Liquid reservoir, 13-minute piping.

Claims (6)

  1. 圧縮機、流路切換手段、凝縮器、絞り機構、および蒸発器が冷媒配管で順次接続され、冷媒が循環する冷媒回路を備え、
    該冷媒回路は、
    前記凝縮器から前記絞り機構へ向かう冷媒と、前記蒸発器から前記圧縮機へ向かう冷媒とを、対向流で熱交換する内部熱交換器を備え、
    該内部熱交換器は、
    内管と外管とからなる二重管構造を有し、
    前記内管は前記凝縮器と前記絞り機構との間に接続され、
    前記外管は前記蒸発器と前記圧縮機との間に接続され
    前記内管の下部に、液冷媒が溜まる液溜め部が設けられており、
    前記液溜め部は、鉛直方向下方に凹んだU字形状を有する
    ことを特徴とする冷凍サイクル装置。
    A compressor, a flow path switching means, a condenser, a throttling mechanism, and an evaporator are sequentially connected by a refrigerant pipe, and include a refrigerant circuit in which the refrigerant circulates;
    The refrigerant circuit is
    An internal heat exchanger that exchanges heat between the refrigerant from the condenser toward the throttle mechanism and the refrigerant from the evaporator toward the compressor in a counterflow;
    The internal heat exchanger is
    It has a double pipe structure consisting of an inner pipe and an outer pipe,
    The inner pipe is connected between the condenser and the throttle mechanism;
    The outer tube is connected between the evaporator and the compressor ;
    A liquid reservoir for storing liquid refrigerant is provided at a lower portion of the inner pipe,
    The refrigeration cycle apparatus characterized in that the liquid reservoir has a U-shape recessed downward in the vertical direction .
  2. 前記液溜め部の上方に、前記内管同士を接続しガス冷媒が通過する分配管が設けられている
    ことを特徴とする請求項に記載の冷凍サイクル装置。
    Above the liquid reservoir, the refrigeration cycle apparatus according to claim 1, characterized in that the distribution pipe the gas refrigerant connecting the inner pipe to each other to pass therethrough.
  3. 前記内管は外径が9.52mmであり、前記外管は、一辺の長さが20cmで外径が15.88mmであり、前記液溜め部は、一辺の長さが20cmで外径が15.88mmの配管を180°曲げて形成されており、前記分配管は、外径が4.8mmである
    ことを特徴とする請求項に記載の冷凍サイクル装置。
    The inner tube has an outer diameter of 9.52 mm, the outer tube has a side length of 20 cm and an outer diameter of 15.88 mm, and the liquid reservoir has a side length of 20 cm and an outer diameter. The refrigeration cycle apparatus according to claim 2 , wherein a 15.88 mm pipe is bent by 180 °, and the distribution pipe has an outer diameter of 4.8 mm.
  4. 前記冷媒回路を室外機に備えた
    ことを特徴とする請求項1〜のいずれか一項に記載の冷凍サイクル装置。
    The refrigeration cycle apparatus according to any one of claims 1 to 3 , wherein the refrigerant circuit is provided in an outdoor unit.
  5. 前記冷媒回路は、
    前記圧縮機と前記凝縮器との間、かつ、前記蒸発器と前記内部熱交換器との間に流路切換手段を備えた
    ことを特徴とする請求項1〜のいずれか一項に記載の冷凍サイクル装置。
    The refrigerant circuit is
    Between said condenser and said compressor, and, according to any one of claims 1 to 4, characterized in that with a passage switching device between said internal heat exchanger and the evaporator Refrigeration cycle equipment.
  6. 前記凝縮器は、プレート式熱交換器である
    ことを特徴とする請求項1〜のいずれか一項に記載の冷凍サイクル装置。
    The refrigeration cycle apparatus according to any one of claims 1 to 5 , wherein the condenser is a plate heat exchanger.
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